JP5997837B2 - Rapid filtration device - Google Patents
Rapid filtration device Download PDFInfo
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- JP5997837B2 JP5997837B2 JP2015513003A JP2015513003A JP5997837B2 JP 5997837 B2 JP5997837 B2 JP 5997837B2 JP 2015513003 A JP2015513003 A JP 2015513003A JP 2015513003 A JP2015513003 A JP 2015513003A JP 5997837 B2 JP5997837 B2 JP 5997837B2
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- 238000001914 filtration Methods 0.000 title claims description 73
- 238000000967 suction filtration Methods 0.000 claims description 48
- 239000007787 solid Substances 0.000 claims description 9
- 239000002245 particle Substances 0.000 claims description 8
- 238000010586 diagram Methods 0.000 description 6
- 238000004519 manufacturing process Methods 0.000 description 6
- 238000000034 method Methods 0.000 description 5
- 239000007788 liquid Substances 0.000 description 2
- 241000894006 Bacteria Species 0.000 description 1
- 230000009286 beneficial effect Effects 0.000 description 1
- 238000006243 chemical reaction Methods 0.000 description 1
- 238000012986 modification Methods 0.000 description 1
- 230000004048 modification Effects 0.000 description 1
- 238000003828 vacuum filtration Methods 0.000 description 1
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Classifications
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/085—Funnel filters; Holders therefor
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/01—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor with flat filtering elements
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D24/00—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof
- B01D24/48—Filters comprising loose filtering material, i.e. filtering material without any binder between the individual particles or fibres thereof integrally combined with devices for controlling the filtration
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/60—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor integrally combined with devices for controlling the filtration
-
- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D29/00—Filters with filtering elements stationary during filtration, e.g. pressure or suction filters, not covered by groups B01D24/00 - B01D27/00; Filtering elements therefor
- B01D29/62—Regenerating the filter material in the filter
- B01D29/66—Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps
- B01D29/668—Regenerating the filter material in the filter by flushing, e.g. counter-current air-bumps with valves, e.g. rotating valves for coaxially placed filtering elements
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- B—PERFORMING OPERATIONS; TRANSPORTING
- B01—PHYSICAL OR CHEMICAL PROCESSES OR APPARATUS IN GENERAL
- B01D—SEPARATION
- B01D37/00—Processes of filtration
- B01D37/04—Controlling the filtration
Description
本発明は濾過技術分野に関し、特に濾過装置の技術分野に関し、具体的には急速濾過装置に関する。 The present invention relates to the field of filtration technology, in particular to the technical field of filtration devices, and in particular to rapid filtration devices.
現在、既知の濾過装置は真空ポンプを採用して減圧濾過を行うものである。真空ポンプの吸気端とフィルタの吸引濾過端とが接続され、真空ポンプに生じる負圧を利用して濾過過程を完成する。然し、この過程で、フィルタが閉塞されやすく、濾過の効率及び速度に影響を与える。 Currently, known filtration devices employ vacuum pumps to perform vacuum filtration. The suction end of the vacuum pump and the suction filtration end of the filter are connected, and the filtration process is completed using the negative pressure generated in the vacuum pump. However, in this process, the filter is likely to become clogged, affecting the efficiency and speed of filtration.
そのため、濾過過程でフィルタを閉塞しにくくすることで、濾過の効率及び速度を向上させる急速濾過装置を提供する必要がある。 Therefore, it is necessary to provide a rapid filtration device that improves the efficiency and speed of filtration by making it difficult to block the filter during the filtration process.
本発明の目的は前記従来技術にある欠点を克服し、設計が巧妙で、構造が簡潔で、濾過過程でフィルタを閉塞させにくくすることで、濾過の効率及び速度を向上させ、大量生産及び広範囲な普及に適する急速濾過装置を提供することにある。 The object of the present invention is to overcome the disadvantages in the prior art, to be cleverly designed, to have a simple structure and to prevent the filter from being blocked during the filtration process, thereby improving the efficiency and speed of filtration, mass production and wide range An object of the present invention is to provide a rapid filtration apparatus suitable for widespread use.
前記目的を実現するために、本発明は、フィルタ及び真空ポンプを含み、前記フィルタの吸引濾過端と前記真空ポンプの吸気端とガス通路で接続される急速濾過装置において、前記吸引濾過端が更に前記真空ポンプの排気端とガス通路で接続され、前記吸気端に生じる負圧によって濾過が行われるように、かつ、前記排気端に生じる正圧によって前記フィルタが吹き返されるように構成され、前記正圧と前記負圧とを交替的に前記フィルタに作用させることで、粒子径の小さい固体によって前記フィルタが閉塞されることを回避することを特徴とする急速濾過装置である。 In order to achieve the above object, the present invention includes a filter and a vacuum pump, wherein the suction filtration end is further connected to the suction filtration end of the filter and the suction end of the vacuum pump by a gas passage. The exhaust pump is connected to the exhaust end of the vacuum pump through a gas passage so that filtration is performed by a negative pressure generated at the intake end, and the filter is blown back by a positive pressure generated at the exhaust end. The rapid filtration apparatus is characterized in that the filter is prevented from being blocked by a solid having a small particle diameter by alternately applying a pressure and a negative pressure to the filter .
好ましくは、前記急速濾過装置は、更に切換弁を含み、前記吸引濾過端が前記切換弁を介して前記吸気端及び前記排気端にそれぞれガス通路で接続される。 Preferably, the rapid filtration device further includes a switching valve, and the suction filtration end is connected to the intake end and the exhaust end via the switching valve through gas passages, respectively.
より好ましくは、前記切換弁は電磁切換弁であり、前記急速濾過装置は更に制御器を含み、前記制御器が前記真空ポンプ及び前記電磁切換弁にそれぞれ電気的に接続する。 More preferably, the switching valve is an electromagnetic switching valve, and the quick filtration device further includes a controller, and the controller is electrically connected to the vacuum pump and the electromagnetic switching valve, respectively.
好ましくは、前記急速濾過装置は更に空気フィルタを含み、前記排気端が前記空気フィルタを介して前記吸引濾過端にガス通路で接続される。 Preferably, the rapid filtration device further includes an air filter, and the exhaust end is connected to the suction filtration end via the air filter through a gas passage.
好ましくは、前記急速濾過装置は更に十字継ぎ手及び三つの停止弁を含み、前記フィルタの数が三つであり、前記吸引濾過端がそれぞれ前記停止弁を介して前記十字継ぎ手にガス通路で接続され、前記十字継ぎ手が前記吸気端及び前記排気端にそれぞれガス通路で接続される。 Preferably, the rapid filtration device further includes a cross joint and three stop valves, the number of the filters is three, and the suction filtration ends are respectively connected to the cross joint through the stop valve by gas passages. The cross joints are connected to the intake end and the exhaust end by gas passages, respectively.
好ましくは、前記停止弁は手動停止弁である。 Preferably, the stop valve is a manual stop valve.
好ましくは、前記フィルタは吸引濾過瓶である。 Preferably, the filter is a suction filter bottle.
好ましくは、前記急速濾過装置は更に第一制御弁及び第二制御弁を含み、前記吸引濾過端が前記第一制御弁及び前記第二制御弁を介して、前記吸気端及び前記排気端にそれぞれガス通路で接続される。 Preferably, the rapid filtration device further includes a first control valve and a second control valve, and the suction filtration end is connected to the intake end and the exhaust end via the first control valve and the second control valve, respectively. Connected by gas passage.
より好ましくは、前記急速濾過装置は更にT字継ぎ手を含み、前記吸引濾過端が前記T字継ぎ手を介して、前記第一制御弁及び前記第二制御弁にそれぞれガス通路で接続される。 More preferably, the rapid filtration device further includes a T-shaped joint, and the suction filtration end is connected to the first control valve and the second control valve via the T-shaped joint, respectively, through gas passages.
好ましくは、前記急速濾過装置は更に第三制御弁、第四制御弁、第五制御弁及び第六制御弁を含み、前記吸引濾過端が前記第四制御弁及び前記第五制御弁を介して前記吸気端及び前記排気端にそれぞれガス通路で接続され、前記吸気端が更に前記第三制御弁にガス通路で接続され、前記排気端が更に前記第六制御弁にガス通路で接続される。 Preferably, the rapid filtration device further includes a third control valve, a fourth control valve, a fifth control valve, and a sixth control valve, and the suction filtration end is connected via the fourth control valve and the fifth control valve. The intake end and the exhaust end are respectively connected by a gas passage, the intake end is further connected to the third control valve by a gas passage, and the exhaust end is further connected to the sixth control valve by a gas passage.
具体的には、本発明の有益な効果は以下のことにある。 Specifically, the beneficial effects of the present invention are as follows.
1.本発明の急速濾過装置はフィルタ及び真空ポンプを含み、前記フィルタの吸引濾過端が前記真空ポンプの吸気端にガス通路で接続され、前記吸引濾過端が更に前記真空ポンプの排気端にガス通路で接続され、濾過過程で、真空ポンプの吸気端と排気端との交替作動を利用し、フィルタに負圧と正圧を交替的に作用させることで、粒子径の小さい固体でフィルタを閉塞することを回避する。これにより、濾過効率及び速度が向上し、設計が巧妙で、構造が簡潔で、濾過過程でフィルタが閉塞されにくいため、濾過の効率及び速度を向上させ、大量生産及び広範囲な普及に適する。 1. The rapid filtration device of the present invention includes a filter and a vacuum pump, the suction filtration end of the filter is connected to the intake end of the vacuum pump through a gas passage, and the suction filtration end is further connected to the exhaust end of the vacuum pump through a gas passage. In the filtration process, the filter is closed with a solid with a small particle diameter by using the alternating action of the suction end and the exhaust end of the vacuum pump to alternately apply negative pressure and positive pressure to the filter. To avoid. As a result, the filtration efficiency and speed are improved, the design is clever, the structure is simple, and the filter is not easily clogged during the filtration process. Therefore, the filtration efficiency and speed are improved, and it is suitable for mass production and widespread use.
2.本発明の急速濾過装置は更に切換弁を含み、前記吸引濾過端が前記切換弁を介して前記吸気端と前記排気端とのそれぞれにガス通路で接続され、切換弁を通じて真空ポンプの吸気端と排気端とが交替的にフィルタの吸引濾過端に連通することを実現するため、設計が巧妙で、構造が簡潔で、濾過過程でフィルタが閉塞されにくいため、濾過の効率及び速度を向上させ、大量生産及び広範囲な普及に適する。 2. The rapid filtration device of the present invention further includes a switching valve, wherein the suction filtration end is connected to each of the intake end and the exhaust end via the switching valve through a gas passage, and through the switching valve, the suction end of the vacuum pump and In order to realize that the exhaust end alternately communicates with the suction filtration end of the filter, the design is clever, the structure is simple, and the filter is not easily blocked during the filtration process, so that the efficiency and speed of filtration are improved, Suitable for mass production and widespread use.
3.本発明の急速濾過装置は更に第一制御弁及び第二制御弁を含み、前記吸引濾過端が前記第一制御弁及び前記第二制御弁を介して前記吸気端及び前記排気端にそれぞれガス通路で接続され、第一制御弁及び第二制御弁を介して真空ポンプの吸気端及び排気端が交替的にフィルタの吸引濾過端に連通することを実現することので、設計が巧妙で、構造が簡潔で、濾過過程で、フィルタが閉塞されにくいため、濾過の効率及び速度を向上させ、大量生産及び広範囲な普及に適する。 3. The rapid filtration apparatus of the present invention further includes a first control valve and a second control valve, and the suction filtration end passes through the first control valve and the second control valve to the intake end and the exhaust end, respectively. And the intake and exhaust ends of the vacuum pump are alternately communicated with the suction filtration end of the filter via the first control valve and the second control valve. Since it is simple and the filter is not easily blocked during the filtration process, it improves the efficiency and speed of filtration and is suitable for mass production and widespread use.
4.本発明の急速濾過装置は更に第三制御弁、第四制御弁、第五制御弁及び第六制御弁を含み、前記吸引濾過端が前記第四制御弁及び前記第五制御弁を介して前記吸気端及び前記排気端にそれぞれガス通路で接続され、前記吸気端が更に前記第三制御弁にガス通路で接続され、前記排気端が更に前記第六制御弁にガス通路で接続され、第四制御弁及び第五制御弁を介して真空ポンプの吸気端及び排気端が交替的にフィルタの吸引濾過端に連通することを実現するので、設計が巧妙で、構造が簡潔で、濾過過程で、フィルタが閉塞されにくいため、濾過の効率及び速度を向上させ、大量生産及び広範囲な普及に適する。 4). The rapid filtration device of the present invention further includes a third control valve, a fourth control valve, a fifth control valve, and a sixth control valve, and the suction filtration end passes through the fourth control valve and the fifth control valve. A gas passage is connected to each of the intake end and the exhaust end, the intake end is further connected to the third control valve via a gas passage, the exhaust end is further connected to the sixth control valve via a gas passage, Since the intake and exhaust ends of the vacuum pump alternately communicate with the suction filtration end of the filter through the control valve and the fifth control valve, the design is clever, the structure is simple, and the filtration process Since the filter is not easily clogged, it improves the efficiency and speed of filtration and is suitable for mass production and widespread use.
本発明の技術内容をより明瞭的に理解できるために、特に以下の実施例を挙げて詳細に説明する。ここで同一部品に同一符号を付する。 In order that the technical contents of the present invention can be understood more clearly, the following examples will be given in detail. Here, the same parts are denoted by the same reference numerals.
図1及び図2の示すように、本発明の急速濾過装置はフィルタ11及び真空ポンプ2を含み、前記フィルタ11の吸引濾過端12と前記真空ポンプ2の吸気端3とがガス通路で接続され、前記吸引濾過端12が更に前記真空ポンプ2の排気端4とガス通路で接続される。使用時、前記吸引濾過端12が前記吸気端3と前記排気端4とに交替的にガス通路で連通される。
As shown in FIGS. 1 and 2, the rapid filtration apparatus of the present invention includes a
前記吸引濾過端12が前記吸気端3と前記排気端4とに交替的に連通することを実現するために、図1及び図2を参照し、本発明の具体的な実施例において、前記急速濾過装置は更に切換弁6を含み、前記吸引濾過端12が前記切換弁6を介して前記吸気端3と前記排気端4とのそれぞれにガス通路で接続される。勿論、前記吸気端3及び前記排気端4が各自の制御弁を介して前記吸引濾過端12にガス通路で接続されても良い。
In order to realize that the
前記切換弁6が手動であってよく、又は電動的であってもよい。図1及び図2を参照し、本発明の具体的な実施例において、前記切換弁6は電磁切換弁であり、前記急速濾過装置は更に制御器1を含み、前記制御器1は前記真空ポンプ2と前記電磁切換弁とにそれぞれ電気的に接続する。 The switching valve 6 may be manually operated or electrically operated. Referring to FIGS. 1 and 2, in a specific embodiment of the present invention, the switching valve 6 is an electromagnetic switching valve, the quick filtration device further includes a controller 1, and the controller 1 is the vacuum pump. 2 and the electromagnetic switching valve are electrically connected to each other.
フィルタ11を保護するために、好ましくは、前記急速濾過装置は更に空気フィルタ5を含み、前記排気端4が前記空気フィルタ5を介して前記吸引濾過端12とガス通路で接続される。図1及び図2の示すように、本発明の具体実施例において、前記空気フィルタ5が前記電磁切換弁を介して前記吸引濾過端12とガス通路で接続させる。
In order to protect the
真空ポンプ2が複数のフィルタ11に接続可能であるために、好ましくは、前記急速濾過装置は更に十字継ぎ手7及び三つの停止弁8、9、10を含み、前記フィルタ11の数が三つ(図1及び図2に一つだけのフィルタ11を示す)とし、前記吸引濾過端12が前記停止弁8、9、10のそれぞれを介して前記十字継ぎ手7にガス通路で接続され、前記十字継ぎ手7が前記吸気端3と前記排気端4とにそれぞれガス通路で接続される。図1及び図2を参照し、本発明の具体的実施例において、前記十字継ぎ手7が前記電磁切換弁を介して前記吸気端3にガス通路で接続され、前記十字継ぎ手7が前記電磁切換弁及び前記空気フィルタ5を介して前記排気端4にガス通路で接続される。
Since the vacuum pump 2 can be connected to a plurality of
前記停止弁8、9、10が手動であってもよく、又は電動であってもよい。前記停止弁8、9、10は、電動の場合、制御器1と電気的に接続できる。図1及び図2を参照し、本発明の具体的な実施例において、前記停止弁8、9、10が手動停止弁である。
The
前記フィルタ11は如何なる適切な部品であっても良く、図1及び図2を参照し、本発明の具体的な実施例において、前記フィルタ11が吸引濾過瓶である。
The
本発明は使用される場合、図1を参照し、制御器1により電磁切換弁を制御することで真空ポンプ2の吸気端3とフィルタ11の吸引濾過端12とを連通させ、真空ポンプ2に生じる負圧をフィルタ11の吸引濾過端12に作用させることで濾過を実現する。図2を参照し、制御器1が電磁切換弁を制御することにより真空ポンプ2の排気端4とフィルタ11の吸引濾過端12とを連通させ、真空ポンプ2に生じる正圧をフィルタ11の吸引濾過端12に作用させることで、粒子径の小さい固体でフィルタ11を閉塞することを回避する。濾過が終了するまで、上記の手順を繰り返す。
When the present invention is used, referring to FIG. 1, the controller 1 controls the electromagnetic switching valve so that the
図3及び図4に本発明の他の具体的な実施例を示し、当該実施例は、図1及び図2に示す具体的な実施例と比較して、切換弁6の機能が第一制御弁14と第二制御弁15により実現される点、即ち、前記吸引濾過端12が、前記第一制御弁14及び前記第二制御弁15を介して前記吸気端3及び前記排気端4にそれぞれガス通路で接続される点で相違する。前記第一制御弁14及び前記第二制御弁15が三方電磁弁であってよい。
3 and 4 show another specific embodiment of the present invention. In this embodiment, the function of the switching valve 6 is controlled first as compared with the specific embodiment shown in FIGS. The point realized by the
前記吸引濾過端12がそれぞれ前記第一制御弁14及び前記第二制御弁15にガス通路で接続するためには、如何なる適切な構造を採用することができる。図3及び図4の表示を参照し、本発明の他の具体実施例において、前記急速濾過装置は更にT字継ぎ手13を含み、前記吸引濾過端12が前記T字継ぎ手13を介して前記第一制御弁14及び前記第二制御弁15にそれぞれガス通路で接続される。
In order to connect the
使用時、図3を参照し、制御器1が前記第一制御弁14及び前記第二制御弁15を制御することで、真空ポンプ2の吸気端3とフィルタ11の吸引濾過端12とを連通させ、真空ポンプ2に生じる負圧をフィルタ11の吸引濾過端12に作用させることにより濾過を実現する。図4を参照し、制御器1が前記第一制御弁14及び前記第二制御弁15を制御することで、真空ポンプ2の排気端4とフィルタ11の吸引濾過端12とを連通させ、真空ポンプ2に生じる正圧をフィルタ11の吸引濾過端12に作用させることにより、粒子径の小さい固体でフィルタ11を閉塞することを回避する。濾過が終了するまで、上記の手順を繰り返す。
In use, referring to FIG. 3, the controller 1 controls the
図5及び図6に本発明の更に他の具体実施例を示し、当該実施例は、図1及び図2に示す具体的な実施例と比較して、切換弁6の機能が第三制御弁16、第四制御弁17、第五制御弁18及び第六制御弁19により実現される点、即ち、前記吸引濾過端12が前記第四制御弁17及び前記第五制御弁18を介して前記吸気端3及び前記排気端4にそれぞれガス通路で接続され、前記吸気端3が更に前記第三制御弁16とガス通路で接続され、前記排気端4が更に前記第六制御弁19とガス通路で接続される点で相違する。第三制御弁16、第四制御弁17、第五制御弁18及び第六制御弁19が二方電磁弁であっても良い。
5 and 6 show still another specific embodiment of the present invention. In this embodiment, the function of the switching valve 6 is the third control valve as compared with the specific embodiment shown in FIGS. 16, the point realized by the
前記吸引濾過端12が前記第四制御弁17及び前記第五制御弁18にそれぞれガス通路で接続するためには、如何なる適切な構造を採用しても良い。前記吸気端3が前記第三制御弁16及び前記第四制御弁17にそれぞれガス通路で接続するためには、如何なる適切な構造を採用しても良い。前記排気端4が前記第五制御弁18及び前記第六制御弁19にそれぞれガス通路で接続するためには、如何なる適切な構造を採用しても良い。図5及び図6の表示を参照し、本発明の更に他の具体的な実施例において、前記急速濾過装置は更に三つのT字継ぎ手13を含み、前記吸引濾過端12がこれら三つのT字継ぎ手13の一つを介して前記第四制御弁17及び前記第五制御弁18にそれぞれガス通路で接続される。前記吸気端3が別のT字継ぎ手13を介して前記第三制御弁16及び前記第四制御弁17にそれぞれガス通路で接続される。前記排気端4が残りのT字継ぎ手13を介して前記第五制御弁18及び前記第六制御弁19にそれぞれガス通路で接続される。
In order to connect the
使用時、図5を参照し、制御器1が前記第四制御弁17及び前記第六制御弁19の開放、並びに前記第三制御弁16及び前記第五制御弁18の閉鎖を制御することで、真空ポンプ2の吸気端3とフィルタ11の吸引濾過端12とを連通させ、真空ポンプ2に生じる負圧をフィルタ11の吸引濾過端12に作用させることで濾過機能を実現する。図6の表示を参照し、制御器1が前記第三制御弁16及び前記第五制御弁18の開放、並びに前記第四制御弁17及び前記第六制御弁19の閉鎖を制御し、真空ポンプ2の排気端4とフィルタ11の吸引濾過端12とを連通させ、真空ポンプ2に生じる正圧をフィルタ11の吸引濾過端12に作用させることで、粒子径の小さい固体でフィルタ11を閉塞することを回避する。濾過が終了するまで、上記の手順を繰り返す。
In use, referring to FIG. 5, the controller 1 controls the opening of the
従って、本発明は急速濾過装置に関し、濾過過程で、まず真空ポンプ2の吸気端3により提供される負圧を利用して濾過を行い、さらに真空ポンプ2の排気端4に生じる正圧を利用してフィルタ11を吹き返し、これにより粒子径の小さい固体でフィルタ11を閉塞することを回避し、また、上記過程は、濾過過程を完成するまで繰り返される。即ち、粒子径の小さい固体でフィルタ11を閉塞することを回避するように、交替的に負圧と正圧とを使用してフィルタ11に作用させることで、濾過効率及び速度を向上させる。本発明は、液体中の固体又は細菌を検出又は除去するために、実験室又は工場等での液体濾過に適用される。
Therefore, the present invention relates to a rapid filtration device, and in the filtration process, first, filtration is performed using the negative pressure provided by the
上述したことから、本発明の急速濾過装置は、設計が巧妙で、構造が簡潔で、濾過過程でフィルタが閉塞されにくいため、濾過の効率及び速度を向上させ、大量生産及び広範囲な普及に適する。 From the above, the rapid filtration apparatus of the present invention has a clever design, a simple structure, and the filter is not easily clogged during the filtration process, thus improving the efficiency and speed of filtration and suitable for mass production and widespread use. .
本明細書には、本発明は既にその特定の実施例を参照して記述されたが、勿論、本発明の精神と範囲を背離せず、種々の修正と変換を行うことができる。そのため、明細書と図面とも限定的でなく説明的であると理解されるべきである。 Although the invention has been described herein with reference to specific embodiments thereof, it will be appreciated that various modifications and conversions can be made without departing from the spirit and scope of the invention. Therefore, it should be understood that the specification and drawings are illustrative rather than limiting.
Claims (10)
前記吸引濾過端が更に前記真空ポンプの排気端とガス通路で接続され、
前記吸気端に生じる負圧によって濾過が行われるように、かつ、前記排気端に生じる正圧によって前記フィルタが吹き返されるように構成され、
前記正圧と前記負圧とを交替的に前記フィルタに作用させることで、粒子径の小さい固体によって前記フィルタが閉塞されることを回避することを特徴とする急速濾過装置。 In a rapid filtration apparatus comprising a filter and a vacuum pump, wherein a suction filtration end of the filter and an intake end of the vacuum pump are connected by a gas passage ,
Before Symbol suction filtration end connected further with an exhaust end and a gas passage of the vacuum pump,
The filter is configured to be filtered by the negative pressure generated at the intake end, and the filter is blown back by the positive pressure generated at the exhaust end,
A rapid filtration apparatus characterized in that the positive pressure and the negative pressure are alternately applied to the filter to prevent the filter from being blocked by a solid having a small particle diameter .
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CN201210162869.7A CN102657966B (en) | 2012-05-23 | 2012-05-23 | Quick suction filtration device |
PCT/CN2013/075842 WO2013174242A1 (en) | 2012-05-23 | 2013-05-17 | Rapid suction-based filtering device |
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Families Citing this family (8)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
CN102657966B (en) * | 2012-05-23 | 2014-07-23 | 宋泳 | Quick suction filtration device |
CN103495300A (en) * | 2013-09-27 | 2014-01-08 | 广州供电局有限公司 | Vacuum filtration device |
CN104841194A (en) * | 2015-05-27 | 2015-08-19 | 吉林大学 | Vacuum suction filtration device |
CN105756592A (en) * | 2016-05-03 | 2016-07-13 | 长江大学 | Negative pressure drilling fluid recovery processing device |
CN106039799A (en) * | 2016-06-30 | 2016-10-26 | 殷霄 | Filtering device for chemical reagent |
CN109365139B (en) * | 2018-10-12 | 2020-10-27 | 北京群动力科技服务有限责任公司 | Continuous flotation method for micro-plastics in different occurrence states in sediment |
CN111908498A (en) * | 2019-12-27 | 2020-11-10 | 深圳市宝安东江环保技术有限公司 | Method for producing copper oxide by using printed circuit board etching waste liquid and electric suction filtration device |
CN114588682B (en) * | 2022-01-12 | 2023-08-04 | 中国矿业大学 | Vacuum filtration-mechanical extrusion integrated coal gasification fine slag continuous dehydration cavity and method |
Family Cites Families (29)
Publication number | Priority date | Publication date | Assignee | Title |
---|---|---|---|---|
JPS5345019B2 (en) * | 1974-09-24 | 1978-12-04 | ||
JPS60139304A (en) * | 1983-12-27 | 1985-07-24 | Tanaka Kikinzoku Kogyo Kk | Suction pipe differential pressure valve apparatus in vacuum suction filter apparatus |
CN2126105U (en) * | 1991-10-10 | 1992-12-30 | 王乃兴 | Filtering and suction filter |
CN1090215A (en) * | 1993-01-29 | 1994-08-03 | 钱志光 | Continuous dual-chamber filter |
DE69513201T2 (en) * | 1995-04-14 | 2000-05-18 | Aquasource Rueil Malmaison | METHOD FOR OPERATING AND CONTROLLING A GROUP OF FILTRATION MEMBRANE MODULES AND A GROUP OF MODULES FOR CARRYING OUT THIS METHOD |
US5578115A (en) * | 1995-07-24 | 1996-11-26 | Devilbiss Health Care, Inc. | Molecular sieve container for oxygen concentrator |
US5879552A (en) * | 1996-01-15 | 1999-03-09 | Bradfield; Michael T. | Method and apparatus for a self-purifying filter system |
US6176897B1 (en) * | 1996-12-31 | 2001-01-23 | Questor Industries Inc. | High frequency pressure swing adsorption |
JP2000189721A (en) * | 1998-12-28 | 2000-07-11 | Ishikawajima Shibaura Mach Co Ltd | Filter device |
US6331251B1 (en) * | 1999-06-10 | 2001-12-18 | Envirogen, Inc. | System and method for withdrawing permeate through a filter and for cleaning the filter in situ |
ES2235983T3 (en) * | 1999-11-18 | 2005-07-16 | Zenon Environmental Inc. | SUBMERGED MEMBRANE FILTRATION SYSTEM AND OVERFLOW PROCESS. |
US6814028B2 (en) * | 2000-03-07 | 2004-11-09 | Nihon University, School Juridical Person | Milking apparatus for laboratory animals |
US6478850B2 (en) * | 2000-08-02 | 2002-11-12 | Wearair Oxygen Inc. | Miniaturized wearable oxygen concentrator |
US6651658B1 (en) * | 2000-08-03 | 2003-11-25 | Sequal Technologies, Inc. | Portable oxygen concentration system and method of using the same |
JP4508443B2 (en) * | 2001-02-22 | 2010-07-21 | 電源開発株式会社 | Coal gasification power plant |
JP4707132B2 (en) * | 2001-06-07 | 2011-06-22 | 日本曹達株式会社 | Suction filtration funnel and suction filtration member |
US7279029B2 (en) * | 2004-05-21 | 2007-10-09 | Air Products And Chemicals, Inc. | Weight-optimized portable oxygen concentrator |
JP4620599B2 (en) * | 2006-02-06 | 2011-01-26 | アクトファイブ株式会社 | Foreign matter removal processing device |
JP5016827B2 (en) * | 2006-02-13 | 2012-09-05 | 三菱レイヨン株式会社 | Membrane separation activated sludge treatment method |
JP5456238B2 (en) * | 2007-02-28 | 2014-03-26 | 三菱レイヨン株式会社 | Membrane separator |
TW200927274A (en) * | 2007-09-18 | 2009-07-01 | Asahi Kasei Chemicals Corp | Hollow yarn film filtering apparatus |
JP5037457B2 (en) * | 2007-09-18 | 2012-09-26 | 旭化成ケミカルズ株式会社 | Drinking water filtration system |
US8695600B2 (en) * | 2009-07-22 | 2014-04-15 | Vbox, Incorporated | Method of separating and distributing oxygen |
CN201482280U (en) * | 2009-08-26 | 2010-05-26 | 宗海宏 | Vacuum continuously-stable guarantee system for pressure reduction and sucking filtration on water solution |
US8181452B2 (en) * | 2009-09-29 | 2012-05-22 | Ford Global Technologies, Llc | Particulate filter regeneration during engine shutdown |
CN102350109A (en) * | 2011-06-27 | 2012-02-15 | 豆远奎 | Filter-cone-type vacuum filtration waste oil device |
CN202212060U (en) * | 2011-07-07 | 2012-05-09 | 中国石油化工股份有限公司 | Filter device |
CN102657966B (en) * | 2012-05-23 | 2014-07-23 | 宋泳 | Quick suction filtration device |
CN202569723U (en) * | 2012-05-23 | 2012-12-05 | 宋泳 | Fast suction filtration device |
-
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